Method for synthesizing nano sapo-34 molecular sieve, and sapo-34 molecular sieve catalyst and application thereof

ABSTRACT

A method for synthesizing a nano SAPO-34 molecular sieve, and an SAPO-34 molecular sieve catalyst and application thereof. A nano SAPO-34 molecular sieve is synthesized by adding a microporous templating agent and a templating agent having a functionalized organic silane to hydrothermal synthesis. The nano SAPO-34 molecular sieve is calcined to obtain a nano SAPO-34 molecular sieve catalyst. The catalyst can be used in a reaction for preparing low-carbon olefin from an oxygen-containing compound. The nano SAPO-34 molecular sieve obtained by this method has a pure CHA crystal phase. Moreover, the nano SAPO-34 molecular sieve catalyst obtained by this method has good catalytic performance in a MTO reaction, the service life of the catalyst is significantly prolonged, and the selectivity of the low-carbon olefin is improved.

TECHNICAL FIELD

The present invention refers to the field of molecular sieves, in particular to a method for synthesizing nano SAPO-34 molecular sieve, a SAPO-34 molecular sieve catalyst and application thereof.

BACKGROUND

The silicoaluminophosphate molecular sieve (SAPO-n) is various in skeleton structure, and its three dimensional skeleton structure is composed of PO₂ ⁺, AlO₂ ⁻ and SiO₂ tetrahedrons. The silicon atoms isomorphously replace part of the P atoms in neutral aluminum phosphate skeleton structure or simultaneously replace P and Al atoms, which makes the skeleton produce net negative charges and causes proton acidity, thus giving the SAPO molecular sieves an acid catalytic performance.

Among them, the SAPO-34 molecular sieve with a CHA topology has been successfully applied in the commercialization of methanol-to-olefin (MTO), due to its excellent catalytic performance in MTO reaction. However, the intrinsic microporous structure of SAPO-34 limits the mass transfer efficiency, resulting in a low utilization rate of active sites of the SAPO-34 catalyst, which leads to channel blockage and carbon deposition deactivation. To solve this problem, the SAPO-34 molecular sieve with a mesoporous-microporous composite structure were synthesized. By introducing mesoporous or macroporous channels among the intrinsic microporous structures or preparing small grains of nano-sized molecular sieve, the mass transfer resistance during reaction was reduced, the molecular diffusion performance during reaction was improved, and the reacting life for catalytic reaction and selectivity to low-carbon olefins were improved.

Triethylamine is an inexpensive and readily available structure-directing agent or template for the synthesis of SAPO-34 molecular sieve. However, when triethylamine is used as a single template, the synthesized product is usually an eutectic crystal of SAPO-34/-18 (CHA/AEI) containing a small amount of SAPO-18. When the silicon content in the synthetic gel is very low or no silicon, a SAPO-18 or AIPO-18 will even be obtained (Micorporous Mesoporous Materials, 2008, 115, 332-337). In addition, the SAPO-34 molecular sieve directed with triethylamine has a larger particle size (3˜5 μm), which limits the molecular mass transfer process in MTO reaction. These are not beneficial to obtaining excellent MTO catalytic reaction results.

SUMMARY OF THE INVENTION

In view of the existing situation above, an object of the present invention is to provide a new method for synthesizing nano SAPO-34 molecular sieve to overcome one or more defects in the prior art.

To this end, in one aspect, the present invention provides a method for synthesizing nano SAPO-34 molecular sieve, wherein synthesizing the nano SAPO-34 molecular sieve by hydrothermal method in the presence of a functionalized organosilane, the functionalized organosilane having the structure shown in Formula I:

wherein n is an integer of 1˜16; R¹ is a C_(1˜10) alkyl group; R² is a C_(1˜6) alkyl group; R³ is a diethylamino, triethylamino, piperazinyl, pyridyl or morpholinyl group; x is an integer of 0˜2, y is an integer of 1˜3, and x+y=3.

In a preferred embodiment, in the Formula I, n is an integer of 3˜8; R¹ and R² are each independently a C_(1˜4) alkyl group; R³ is a piperazinyl, pyridyl or morpholinyl group.

In a preferred embodiment, the method comprises the following steps:

a) dissolving the functionalized organosilane in water, and then adding sequentially an aluminum source, a phosphorus source, an organic amine and an additional silicon source to obtain a mixture with the following molar ratio: SiO₂:P₂O₅:Al₂O₃:organic amine:H₂O=0.2˜1.2:0.5˜1.5:0.6˜1.4:1.5˜5.5:50˜200; b) crystallizing the mixture obtained from step a) for 0.4˜10 days at 150˜220° C.; c) after the crystallization of step b), separating the solid product, and washing and drying it to obtain the nano SAPO-34 molecular sieve.

In a preferred embodiment, the molar ratio of the functionalized organosilane to the additional silicon source in the mixture obtained from step a) is 1˜55:10, based on the molar number of SiO₂.

In a preferred embodiment, in step a), the phosphorus source is one or more selected from orthophosphoric acid, metaphosphoric acid, phosphate and phosphite; the aluminum source is one or more selected from aluminum salt, active alumina, alkoxy aluminum and metakaolin; the additional silicon source is one or more selected from silica sol, active silica, orthosilicate and metakaolin.

In a preferred embodiment, in step a), the organic amine is one or more selected from triethylamine, tetraethylammonium hydroxide, morpholine, diethylamine, di-n-propylamine and diisopropylamine.

In a preferred embodiment, in step a), the organic amine is triethylamine.

In a preferred embodiment, in step b), the time for the crystallization is 1˜7 days.

In another aspect, the present invention provides a SAPO-34 molecular sieve catalyst, wherein the SAPO-34 molecular sieve catalyst is obtained by calcining the nano SAPO-34 molecular sieve synthesized according to the above-described method in air at 400˜700° C.

In yet another aspect, the present invention provides the application of the SAPO-34 molecular sieve catalyst in the conversion of oxygenated compounds to low-carbon olefins, wherein the oxygenated compounds are C_(1˜4) alcohols and the low-carbon olefins are C_(2˜6) olefins.

The advantageous effects of the present invention include but are not limited to:

(1) the nano SAPO-34 molecular sieve obtained by the method of the present invention has a small primary particle size (about 50 nm˜200 nm), a large external specific surface area (about 80 m²/g˜100 m²/g) and a large mesoporous volume (about 0.10 m³/g˜0.25 m³/g); (2) the nano SAPO-34 molecular sieve obtained by the method of the present invention has a pure CHA crystal phase; (3) the SAPO-34 molecular sieve catalyst obtained by the method of the invention exhibits an excellent catalytic performance in MTO reaction, of which the service life is significantly prolonged and the selectivity to low-carbon olefins is improved.

DESCRIPTION OF THE FIGURES

FIG. 1 is a SEM image of the nano SAPO-34 molecular sieve sample obtained according to Example 1 of the present application.

FIG. 2 is a SEM image of the SAPO-34 molecular sieve sample obtained according to Comparative Example 1 of the present application.

FIG. 3 is a XRD diffraction pattern of the SAPO-34 molecular sieve samples obtained according to Example 1 and Comparative Examples 1˜3 of the present application.

DETAILED DESCRIPTION OF THE EMBODIMENT

According to one aspect, the present application provides a method for synthesizing nano SAPO-34 molecular sieve by hydrothermal method with assistance of a functionalized organosilane. The functions of the functionalized organosilane in the synthesis are at least in the following three aspects: 1) as a crystal growth inhibitor to reduce crystal size; 2) as an organic silicon source; 3) the functional groups of the functionalized organosilane have partly a structure-directing effect to inhibit the SAPO-18 eutectic crystal produced by using such as triethylamine as a microporous template, and thus the nano SAPO-34 molecular sieve with a pure CHA crystal phase is successfully synthesized.

In the present invention, the obtained nano SAPO-34 molecular sieves are usually an aggregate of nanoparticles.

In the present invention, the functionalized organosilane is selected from at least one of the alkoxy organosilane compounds containing diethylamino, triethylamino, piperazinyl, pyridyl or morpholinyl groups. Among them, the alkoxy organosilane may generally be regarded as an organosilicon compound composed of silicon atoms directly connected with 1˜4 alkoxy groups. The diethylamino group is a group obtained by losing hydrogen atom on the nitrogen atom in diethylamine molecule. The triethylamino group is a group obtained by losing hydrogen atom on the nitrogen atom in triethylamine molecule. The piperazinyl group is a group obtained by losing hydrogen atom on a nitrogen atom in the six-membered cyclic piperazine molecule. The pyridyl group is a group obtained by losing hydrogen atom on the nitrogen atom or any carbon atom in the six-membered cyclic piperazine molecule. The morpholinyl group is a group obtained by losing hydrogen atom on the nitrogen atom or any carbon atom in the six-membered cyclic morpholine molecule.

Preferably, the functionalized organosilane has the structure shown in Formula I:

wherein n is an integer of 1˜16; R¹ is a C_(1˜10) alkyl group; R² is a C_(1˜6) alkyl group; R³ is a diethylamino, triethylamino, piperazinyl, pyridyl or morpholinyl group; x is an integer of 0˜2, y is an integer of 1˜3, and x+y=3. More preferably, n is an integer of 3˜8; R¹ and R² are each independently a C_(1˜4) alkyl group; R³ is a piperazinyl, pyridyl or morpholinyl group.

In the present invention, the alkyl group is a group formed by losing any hydrogen atom in any linear or branched saturated alkane molecule.

In the present invention, preferably, the method for synthesizing nano SAPO-34 molecular sieve comprises the following synthetic steps:

a) dissolving the functionalized organosilane in water, and then adding sequentially an aluminum source, a phosphorus source, an organic amine and an additional silicon source (i.e. organic silicon source or inorganic silicon source) to obtain a mixture with the following molar ratio (the addition amount of the functionalized organosilane and the additional silicon source is based on the molar number of SiO₂, the addition amount of the phosphorus source is based on the molar number of P₂O₅, and the addition amount of the aluminum source is based on the molar number of Al₂O₃): SiO₂:P₂O₅:Al₂O₃:organic amine:H₂O=0.2˜1.2:0.5˜1.5:0.6˜1.4:1.5˜5.5:50˜200; b) crystallizing the mixture obtained from step a) for 0.4˜10 days at 150˜220° C.; c) after the crystallization of step b) is completed, separating the solid product, and washing and drying it to obtain the nano SAPO-34 molecular sieve.

The above-described method may be carried out in a conventional reactor for hydrothermally synthesizing molecular sieves, such as a crystallization reactor.

Preferably, in the mixture obtained from step a), the molar ratio of the functionalized organosilane to the additional silicon source (functionalized organosilane: additional silicon source) is 1˜55:10, based on the molar number of SiO₂. More preferably, the functionalized organosilane: additional silicon source is 1˜15:3.

Preferably, in step a), the inorganic phosphorus compound is selected from at least one of orthophosphoric acid, metaphosphoric acid, phosphate and phosphite.

Preferably, in step a), the aluminum source is selected from at least one of aluminum isopropoxide, pseudoboehmite and aluminum hydroxide.

Preferably, in step a), the additional silicon source is selected from at least one of silica sol, active silica, orthosilicate and metakaolin.

Preferably, in step a), the organic amine is one or more selected from triethylamine, tetraethylammonium hydroxide, morpholine, diethylamine, di-n-propylamine and diisopropylamine. More preferably, in step a), the organic amine is selected from triethylamine (abbreviated as TEA).

Preferably, in step b), the time for the crystallization is 1˜7 days.

As a preferred embodiment, the method for synthesizing nano SAPO-34 molecular sieve comprises the following steps:

1) dissolving the functionalized organosilane in water and stirring at room temperature for 4˜24 hours; 2) adding subsequently an aluminum source, a phosphorus source, an organic amine and an additional silicon source to the solution from step 1) and stirring at room temperature for 1˜24 hours, with the molar ratio of respective component in the mixed solution being as follows: (0.2˜1.2) SiO₂: (0.5˜1.5) P₂O₅: (0.6˜1.4) Al₂O₃: (1.5˜5.5) organic amine: (50˜200) H₂O, wherein the molar ratio of the functionalized organosilane to the additional silicon source is 1˜15:3; 3) crystallizing the mixed solution of step 2) for 0.4˜10 days at 150˜220° C.; 4) after the crystallization of step 3), separating the solid product by centrifugation, washing it with deionized water to neutral, and drying it in air at 120° C. to obtain the nano SAPO-34 molecular sieve raw powder.

According to another aspect, the present application provides a SAPO-34 molecular sieve catalyst (or acid catalyst), wherein the SAPO-34 molecular sieve catalyst is obtained by calcining the nano SAPO-34 molecular sieve synthesized according to any of the above-described methods in air at 400˜700° C.

According to yet another aspect, the present application provides the application of the SAPO-34 molecular sieve catalyst in the conversion of oxygenated compounds to olefins.

EXAMPLES

Hereinafter, the present application is illustrated in detail by way of Examples, but the present application is not limited to these Examples.

Unless specially stated otherwise, the test conditions in the present application are as follows:

Elemental composition was determined on Magix-601 type X-ray fluorescence analyzer (XRF) (Philips company).

X-ray powder diffraction phase analysis (XRD) was conducted on X′Pert PRO type X-ray diffractometer from PANalytical company of the Netherlands, Cu target, Ku radiation source (X=0.15418 nm), voltage 40 KV, current 40 mA.

SEM morphology was analyzed on SU8020 type scanning electron microscope from the scientific instrument factory of the Chinese Academy of Sciences.

N₂ physical adsorption analysis was determined on Micromeritics ASAP 2020 type physical adsorption analyzer from Mike company of USA.

The functionalized organosilane and n-octyl trimethoxysilane used in the Examples were purchased from Shanghai Dibai Chemical Technology Co., Ltd. Octadecyl dimethyl trimethoxysilyl propyl ammonium chloride was purchased from Sigma Aldridge (Shanghai) Co., Ltd. As a nonrestrictive example, in Formula I, R¹ is methyl; R² is methyl; R³ is any one of piperazinyl, pyridyl and morpholinyl groups; x=1; y=2; n=3˜8; and the functionalized organosilane with R³ being piperazinyl group is abbreviated as PiSi-n; the functionalized organosilane with R³ being pyridyl group is abbreviated as BiSi-n; the functionalized organosilane with R³ being morpholinyl group is abbreviated as MoSi-n, wherein the n takes the value of corresponding n. For example, “PiSi-3” denotes the functionalized organosilane compound with a chemical structure of n=3, R¹ is methyl, R² is methyl, R³ is piperazinyl, x=1 and y=2 in Formula I.

Example 1

The molar ratio of respective raw materials, the crystallization condition and the elemental composition are shown in Table 1. The specific batching process is as follows:

9.28 g PiSi-3 and 71.40 g deionized water were mixed and stirred for 1 hour, then 135.64 g pseudoboehmite (72.5% Al₂O₃, mass percentage content), 34.58 g phosphoric acid (85% H₃PO₄, mass percentage content), 20.24 g triethylamine and 8.33 g tetraethyl orthosilicate were added sequentially, followed by being stirred and aged for 24 hours. Subsequently, the gel mixture was transferred into a stainless steel reactor. The molar ratio of respective component in the synthesis system is 0.8 SiO₂:1.5P₂O₅:0.8 Al₂O₃:2 TEA:80 H₂O, and the molar ratio of PiSi-3 to tetraethyl orthosilicate is 1:1.

After the reactor was put into an oven, the programmed temperature was raised to 200° C., and the static crystallization was carried out for 48 h. After the reaction, the solid product was centrifuged, washed repeatedly with deionized water, and dried in air at 120° C. to obtain the nano SAPO-34 molecular sieve sample.

The morphology of the obtained sample was characterized by scanning electron microscopy. The electron microscopic photograph of the sample is shown in FIG. 1. The obtained sample assumes spherical micron particles aggregated from strip-like nanocrystals. The particle size distribution of the strip-like nanocrystals is between 50 nm˜200 nm. The results of XRD analysis are shown in FIG. 3 and Table 2. The results show that the synthesized product has a pure SAPO-34 crystal phase.

The elemental composition of the obtained sample was analyzed by XRF. The results are shown in Table 1.

Comparative Example 1

The batching proportion and synthesis process were the same as in Example 1, but no piperazine-based organosilane PiSi-3 was added, and the piperazine-based organosilane PiSi-3 in Example 1 was replaced by tetraethyl orthosilicate with SiO₂ of the same molar number.

The morphology of the sample obtained in Comparative Example 1 was characterized by scanning electron microscopy. The electron microscopic photograph of the sample is shown in FIG. 2, indicating that the sample assumes smooth cubic large grains with a particle size of about 5 μm.

The XRD diffraction pattern of the raw powder of the sample in Comparative Example 1 is also shown in FIG. 3. The results show that the sample in Comparative Example 1 has obvious broad peaks at 16-17.5°, 21-22.5° and 30-32°, indicating that the sample in Comparative Example 1 is a SAPO-34/-18 eutectic crystal with a relatively higher content of SAPO-34 (for the specific content analysis for respective crystal phase, referring to the website of International Molecular Sieve Association, http://www.iza-online.org/default.htm).

Comparative Example 2

The batching proportion and synthesis process were the same as in Example 1, but no piperazine-based organosilane PiSi-3 was added, and the piperazine-based organosilane PiSi-3 in Example 1 was replaced by a quaternary ammonium surfactant of octadecyl dimethyl trimethoxysilyl propyl ammonium chloride (TPOAC) with SiO₂ of the same molar number.

The XRD diffraction pattern of the raw powder of the sample in Comparative Example 2 is shown in FIG. 3. The diffraction pattern indicates that the sample using TPOAC in Comparative Example 2 contains a SAPO-18 eutectic crystal.

Comparative Example 3

The batching proportion and synthesis process were the same as in Example 1, but no piperazine-based organosilane PiSi-3 was added, and the piperazine-based organosilane PiSi-3 in Example 1 was replaced by n-octyl trimethoxysilane, which has no organic functional groups, with P₂O₅ of the same molar number.

The XRD diffraction pattern of the raw powder of the sample in Comparative Example 3 is shown in FIG. 3. The diffraction pattern indicates that the sample using n-octyl trimethoxysilane in Comparative Example 3 contains a SAPO-18 eutectic crystal.

Examples 2˜12

The specific batching proportions and crystallization conditions are shown in Table 1, and the specific batching processes are the same as in Example 1.

The results of XRD analysis for the samples obtained in Examples 2˜12 are similar to those in table 2, that is, the positions and shapes of the peaks are the same, and the relative peak intensities of the peaks fluctuate within a range of ±10% according to the variation in synthetic condition, indicating that the synthesized products have the characteristics of SAPO-34 structure.

The XRF elemental compositions of the samples in Examples 2˜12 were analyzed, and the results are shown in Table 1.

The morphologies of the samples in Examples 2˜12 were analyzed by scanning electron microscopy, and the obtained electron microscopic photographs are similar to that in FIG. 1.

TABLE 1 Synthesis batching, crystallization condition and elemental composition of molecular sieves Additional Phosphorus Organosilane silicon source Aluminum Organic and source and and P₂O₅ source and amine H₂O Crystal- Crystal- Exam- SiO₂ molar SiO₂ molar molar Al₂O₃ molar molar molar lization lization Elemental composition ple number number number number number number temperature time analysis result of product 1 PiSi-3 tetraethyl orthophosphoric pseudoboehmite 0.20 mol  8.0 mol 200° C. 48 h (Si_(0.14)Al_(0.45)P_(0.41))O₂ 0.04 mol orthosilicate acid 0.08 mol 0.04 mol 0.15 mol 2 BiSi-3 silica sol orthophosphoric aluminum 0.45 mol  5.5 mol 210° C. 60 h (Si_(0.15)Al_(0.45)P_(0.40))O₂ 0.02 mol 0.06 mol acid isopropoxide 0.12 mol 0.12 mol 3 MoSi-4 carbon-white orthophosphoric aluminum 0.35 mol 15.0 mol 180° C. 96 h (Si_(0.06)Al_(0.48)P_(0.46))O₂ 0.01 mol 0.01 mol acid isopropoxide 0.05 mol 0.06 mol 4 BiSi-7 tetraethyl orthophosphoric aluminum 0.15 mol 20.0 mol 200° C. 24 h (Si_(0.17)Al_(0.45)P_(0.38))O₂ 0.04 mol orthosilicate acid hydroxide 0.08 mol 0.08 mol 0.12 mol 5 PiSi-4 carbon-white metaphosphoric aluminum 0.20 mol  5.0 mol 190° C. 120 h  (Si_(0.04)Al_(0.55)P_(0.41))O₂ 0.05 mol 0.03 mol acid hydroxide 0.10 mol 0.14 mol 6 PiSi-5 silica sol metaphosphoric pseudoboehmite 0.55 mol 10.0 mol 150° C. 168 h  (Si_(0.08)Al_(0.49)P_(0.43))O₂ 0.01 mol 0.03 mol acid 0.08 mol 0.08 mol 7 MoSi-8 silica sol ammonium pseudoboehmite 0.20 mol 12.0 mol 210° C. 48 h (Si_(0.10)Al_(0.47)P_(0.43))O₂ 0.02 mol 0.04 mol hydrogen 0.12 mol phosphate 0.09 mol 8 PiSi-6 tetraethyl metaphosphoric aluminum 0.28 mol  9.0 mol 200° C. 96 h (Si_(0.18)Al_(0.45)P_(0.37))O₂ 0.05 mol orthosilicate acid isopropoxide 0.06 mol 0.05 mol 0.12 mol 9 MoSi-6 carbon-white Ammonium pseudoboehmite 0.35 mol 16.0 mol 220° C. 12 h (Si_(0.19)Al_(0.44)P_(0.37))O₂ 0.10 mol 0.02 mol dihydrogen 0.10 mol phosphate 0.12 mol 10 PiSi-3 tetraethyl Ammonium pseudoboehmite 0.40 mol 20.0 mol 200° C. 48 h (Si_(0.12)Al_(0.46)P_(0.42))O₂ 0.03 mol orthosilicate dihydrogen 0.12 mol 0.04 mol phosphate 0.10 mol 11 PiSi-4 silica sol orthophosphoric aluminum 0.30 mol 10.5 mol 190° C. 24 h (Si_(0.13)Al_(0.48)P_(0.39))O₂ 0.05 mol 0.05 mol acid hydroxide 0.10 mol 0.07 mol 12 BiSi-8 carbon-white metaphosphoric aluminum 0.50 mol 16.0 mol 160° C. 36 h (Si_(0.10)Al_(0.46)P_(0.44))O₂ 0.02 mol 0.04 mol acid isopropoxide 0.08 mol 0.10 mol

TABLE 2 XRD results of sample obtained in Example 1 No. 2θ d (Å) 100 * I/I₀ 1 9.493116 9.31665 92.35 2 12.84392 6.89261 28.9 3 13.99115 6.32991 6.72 4 15.99025 5.54277 47.72 5 17.93924 4.94473 20.31 6 20.55734 4.32053 100 7 22.18501 4.00708 6.43 8 23.05264 3.8582 6.76 9 25.16641 3.53873 23.32 10 25.85266 3.44633 25.98 11 27.61156 3.2302 4.38 12 29.48936 3.02908 3.57 13 30.5581 2.92553 41.07 14 31.15588 2.87075 20.74 15 34.45969 2.60271 8.54 16 36.22659 2.47972 3.39 17 39.63702 2.27387 3.8 18 43.40979 2.08459 5.02 wherein θ represents the XRD diffraction angle, d represents the interplanar crystal spacing, I represents the relative diffraction peak intensity, and I₀ represents the relative maximum diffraction peak intensity.

Example 13

The samples obtained in Examples 1˜4 and Comparative Example 1 were calcined in air at 600° C. for 4 hours, and then subject to N₂ physical adsorption analysis. The results are shown in Table 3. From the results in Table 3, it can be seen that the samples obtained in Examples 1 to 4 have significantly increased external specific surface area and mesoporous volume, compared with the data from Comparative Example 1.

TABLE 3 Specific surface area and pore volume of samples Specific surface area (m²/g) V_(micropore) V_(mesopore) ^(b) Sample S_(BET) S_(micropore) ^(a) S_(mesopore) (cm³/g) (cm³/g) Comparative 572 566 6 0.24 0.01 Example 1 Example 1 577 478 99 0.22 0.17 Example 2 577 475 102 0.22 0.18 Example 3 582 493 89 0.23 0.13 Example 4 597 488 109 0.22 0.17 ^(a)calculated by t-plot method ^(b)calculated by BJH method wherein V_(micropore) represents the volume of micropores in material, S_(BET) represents the BET surface area of material, S_(micropore) represents the specific surface area of micropores in material, and S_(mesopore) represents the specific surface area of mesopores in material

Example 14

The samples obtained in Examples 1˜4 and Comparative Example 1 were calcined in air at 600° C. for 4 hours, and then tableted and crushed to 40˜60 meshes. 0.3 g of each sample was charged into a fixed bed reactor and subject to MTO reaction for evaluation. The sample was activated for 1 hour at 550° C. under nitrogen, and then cooled to 450° C. for the reaction. Methanol was carried by nitrogen. The flow rate of nitrogen was 42 ml/min, and the mass hourly space velocity of methanol was 4 h⁻¹. The reaction products were analyzed by on-line gas chromatography (Varian 3800, FID detector, capillary column PoraPLOT Q-HT). The results are shown in Table 4.

Table 4: Reaction Results of Samples for Conversion of Methanol to Olefins

TABLE 4 Reaction results of samples for conversion of methanol to olefins Service Selectivity (mass %) Sample life (min) ^(a) CH₄ C₂H₄ C₂H₆ C₃H₆ C₃H₈ C₂H₄ + C₃H₆ ^(b) C₄-C₆ Comparative 160 3.89 44.40 0.72 32.12 1.81 76.51 17.06 Example 1 Example 1 330 2.04 49.37 0.39 33.65 0.60 83.02 13.92 Example 2 300 2.24 50.15 0.46 32.93 0.67 83.07 13.54 Example 3 460 1.23 50.19 0.41 34.83 0.74 85.02 9.87 Example 4 360 2.24 49.87 0.47 32.88 0.76 82.76 13.76 ^(a)The reaction time during which the conversion of methanol was 100%. ^(b)The highest (ethylene + propylene) selectivity when the conversion of methanol was 100% a. The reaction time during which the conversion of methanol was 100%. b. The highest (ethylene+propylene) selectivity when the conversion of methanol was 100%.

Although the present application is disclosed with preferred embodiments as above, it does not mean that the present application is limited by them. Without departing from the inventive concept of the present application, any slight variations and modifications made by those skilled in the art who is familiar with this major by utilizing the above disclosures are all equal to the equivalent embodiments and fall into the scope of the technical solutions of the present application. 

1-10. (canceled)
 11. A method for synthesizing nano SAPO-34 molecular sieve, the method comprising: synthesizing the nano SAPO-34 molecular sieve by hydrothermal method in the presence of a functionalized organosilane, the functionalized organosilane having the structure shown in Formula I:

wherein n is an integer ranging from 1 to 16; R¹ is selected from C_(1˜10) alkyl group; R² is selected from C_(1˜6) alkyl group; R³ is selected from diethylamino, triethylamino, piperazinyl, pyridyl or morpholinyl group; x is an integer ranging from 0 to 2, y is an integer ranging from 1 to 3, and x+y=3.
 12. The method according to claim 11, wherein in the Formula I, n is an integer ranging from 3 to 8; R¹ and R² are each independently selected from C_(1˜4) alkyl group; R³ is selected from piperazinyl, pyridyl or morpholinyl group.
 13. The method according to claim 11, wherein the method comprises the following steps: a) dissolving the functionalized organosilane in water, and then adding sequentially an aluminum source, a phosphorus source, an organic amine and an additional silicon source to obtain a mixture with the following molar ratio: SiO₂:P₂O₅:Al₂O₃:organic amine:H₂O=0.2˜1.2:0.5˜1.5:0.6˜1.4:1.5˜5.5:50˜200; b) crystallizing the mixture obtained from step a) for a crystallization time in a range from 0.4 to 10 days at a crystallization temperature in a range from 150 to 220° C.; c) after the crystallization of step b), separating the solid product, and washing and drying it to obtain the nano SAPO-34 molecular sieve.
 14. The method according to claim 13, wherein the molar ratio of the functionalized organosilane to the additional silicon source in the mixture obtained from step a) is 1˜55:10, based on the molar number of SiO₂.
 15. The method according to claim 13, wherein in step a), the phosphorus source is one or more selected from orthophosphoric acid, metaphosphoric acid, phosphate and phosphite; the aluminum source is one or more selected from aluminum salt, active alumina, alkoxy aluminum and metakaolin; the additional silicon source is one or more selected from silica sol, active silica, orthosilicate and metakaolin.
 16. The method according to claim 13, wherein in step a), the organic amine is one or more selected from triethylamine, tetraethylammonium hydroxide, morpholine, diethylamine, di-n-propylamine and diisopropylamine.
 17. The method according to claim 13, wherein in step a), the organic amine is triethylamine.
 18. The method according to claim 13, wherein in step b), the crystallization time is in a range from 1 to 7 days.
 19. A SAPO-34 molecular sieve catalyst, wherein the SAPO-34 molecular sieve catalyst is obtained by calcining the nano SAPO-34 molecular sieve synthesized by the method according to any one of claim 11 in air at a temperature in a range from 400 to 700° C.
 20. A SAPO-34 molecular sieve catalyst, wherein the SAPO-34 molecular sieve catalyst is obtained by calcining the nano SAPO-34 molecular sieve synthesized by the method according to claim 12 in air at a temperature in a range from 400 to 700° C.
 21. A SAPO-34 molecular sieve catalyst, wherein the SAPO-34 molecular sieve catalyst is obtained by calcining the nano SAPO-34 molecular sieve synthesized by the method according to claim 13 in air at a temperature in a range from 400 to 700° C.
 22. A SAPO-34 molecular sieve catalyst, wherein the SAPO-34 molecular sieve catalyst is obtained by calcining the nano SAPO-34 molecular sieve synthesized by the method according to claim 14 in air at a temperature in a range from 400 to 700° C.
 23. A SAPO-34 molecular sieve catalyst, wherein the SAPO-34 molecular sieve catalyst is obtained by calcining the nano SAPO-34 molecular sieve synthesized by the method according to claim 15 in air at a temperature in a range from 400 to 700° C.
 24. A SAPO-34 molecular sieve catalyst, wherein the SAPO-34 molecular sieve catalyst is obtained by calcining the nano SAPO-34 molecular sieve synthesized by the method according to claim 16 in air at a temperature in a range from 400 to 700° C.
 25. A SAPO-34 molecular sieve catalyst, wherein the SAPO-34 molecular sieve catalyst is obtained by calcining the nano SAPO-34 molecular sieve synthesized by the method according to claim 17 in air at a temperature in a range from 400 to 700° C.
 26. A SAPO-34 molecular sieve catalyst, wherein the SAPO-34 molecular sieve catalyst is obtained by calcining the nano SAPO-34 molecular sieve synthesized by the method according to claim 18 in air at a temperature in a range from 400 to 700° C.
 27. Application of the SAPO-34 molecular sieve catalyst according to claim 19 in the conversion of oxygenated compounds to low-carbon olefins, wherein the oxygenated compounds are selected from C_(1˜4) alcohols and the low-carbon olefins are C_(2˜6) olefins. 